Classifications

• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L21/00—Compositions of unspecified rubbers
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L19/00—Compositions of rubbers not provided for in groups C08L7/00 - C08L17/00
  • C08L19/003—Precrosslinked rubber; Scrap rubber; Used vulcanised rubber
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
  • C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
  • C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
  • C08L23/04—Homopolymers or copolymers of ethene
  • C08L23/06—Polyethene
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
  • C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
  • C08L23/10—Homopolymers or copolymers of propene
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
  • C08K5/00—Use of organic ingredients
  • C08K5/04—Oxygen-containing compounds
  • C08K5/09—Carboxylic acids; Metal salts thereof; Anhydrides thereof
  • C08K5/098—Metal salts of carboxylic acids
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
  • C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
  • C08L23/04—Homopolymers or copolymers of ethene
  • C08L23/08—Copolymers of ethene
  • C08L23/0846—Copolymers of ethene with unsaturated hydrocarbons containing other atoms than carbon or hydrogen atoms
  • C08L23/0853—Vinylacetate
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
  • C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
  • C08L23/04—Homopolymers or copolymers of ethene
  • C08L23/08—Copolymers of ethene
  • C08L23/0846—Copolymers of ethene with unsaturated hydrocarbons containing other atoms than carbon or hydrogen atoms
  • C08L23/0869—Acids or derivatives thereof
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
  • C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
  • C08L23/10—Homopolymers or copolymers of propene
  • C08L23/12—Polypropene
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L53/00—Compositions of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L61/00—Compositions of condensation polymers of aldehydes or ketones; Compositions of derivatives of such polymers
  • C08L61/04—Condensation polymers of aldehydes or ketones with phenols only
  • C08L61/06—Condensation polymers of aldehydes or ketones with phenols only of aldehydes with phenols

Definitions

• This invention relates to improved polymer blends of ground vulcanized rubber and polyolefin resin, and in particular, blends of enhanced compatibility due to the presence of a functionalized olefin polymer.
• Blends of ground vulcanized rubber and thermoplastic polymer are known. for example, in U.S. Pat. No. 4,028,288, a method is described for preparing mixtures of vulcanized rubber particles and a thermoplastic polymer.
• a method is described for preparing mixtures of vulcanized rubber particles and a thermoplastic polymer.
• the resulting compositions exhibited poor mechanical properties, especially low elongation. Therefore, if the compatibility of the blend components can be increased, improved compositions would be obtained.
• thermoplastic elastomeric composition consisting of comminuted vulcanized rubber, a thermoplastic olefin or diolefin polymer, and a compatibilizer additive.
• the compatibilizer additive is the reaction product of hydroxyl compound with an alkene oxide.
• the mechanical properties of such composition e.g., percent elongation at break
• compositions comprising a blend of ground vulcanized rubber and a polyolefin resin is obtained by the incorporation therein, of a functionalized olefin polymer.
• Blends containing high proportions of ground vulcanized rubber are elastoplastic, which means they are elastomeric, but can be processed as a thermoplastic. The melt processability of these compositions allows shaped articles of these compositions to be molded therefrom without the time consuming cure step required with conventional rubbers, thereby reducing finished part cost.
• improved compatibilized polymer blends comprise (a) ground vulcanized rubber in the form of small dispersed particles specifically of 1.5 mm number average or below, (b) polyolefin resin, (c) functionalized olefin polymer, and if desired, additives such as fillers, pigments, reinforcements, stabilizers, processing aids, colorants, plasticizers and other compounding or modifying ingredients which may be included in order to meet specific performance needs of each customer.
• Component (a) is mechanically or cryogenically ground vulcanized rubber in the form of small particles essentially of 1.5 mm number average or below and more preferably a particle size between 0.1 mm and 1.0 mm number average.
• exemplary of the vulcanized rubber include natural rubber, synthetic polymer of copolymer rubber derived from alkadienes, or mixtures thereof. For economic reasons, vulcanized rubber from scrap tires, retreaded tire buffings, tire tubes, and miscellaneous waste thermoset rubber articles is especially preferred for purposes of the subject invention.
• the polyolefin resin listed as component (b) is a solid, high molecular weight polymeric material made by polymerizing one or more olefinic monomers in a conventional manner.
• olefins are ethylene, propylene, 1-butene, 1-pentene, 2-methyl-1 propene, or mixtures thereof.
• Preferred polyolefin resins are polyethylene or polypropylene.
• the functionalized olefin polymer listed as component (c) is a copolymer of at least one olefin and one or more ethylenically unsaturated organic monomers.
• Preferred olefins include ethylene, propylene, butylene, butadiene, isoprene, including hydrogenated butadiene or isoprene.
• organic monomers examples include those selected from the group consisting of unsaturated mono or dicarboxylic acids of 3-20 carbon atoms and their derivatives such as acid anhydrides, maleamic acids, acid halides, esters, metal salts and the like; vinyl esters of saturated carboxylic acids where the acid group has 2-18 carbon atoms, vinyl alkyl ethers wherein the alkyl group has 1-18 carbon atoms, vinyl or vinylidene halides, acrylonitrile, methacrylonitrile, and vinyl aromatic compounds.
• unsaturated mono or dicarboxylic acids of 3-20 carbon atoms and their derivatives such as acid anhydrides, maleamic acids, acid halides, esters, metal salts and the like
• vinyl esters of saturated carboxylic acids where the acid group has 2-18 carbon atoms
• vinyl alkyl ethers wherein the alkyl group has 1-18 carbon atoms
• vinyl or vinylidene halides vinylonitrile, methacrylonitrile, and vinyl aromatic
• Preferred functionalized olefin polymers contain at least one olefin, including hydrogenated butadiene or isoprene, modified by a reactive functional group such as carboxylic acid or its derivatives.
• the functional groups may be either (i) on the polymer backbone such as in copolymers or ethylene and acrylic acid available from Dow Chemical Company under the trade name Primacor or (ii) grafted onto the main polymer backbone, examples of which are polypropylene grafted with maleic acid anhydride available from Hercules-Himont as Hercoprime and polypropylene grafted with acrylic acid available from BP Performance Polymers, Inc. under the trade name Polybond.
• the amount of organic monomer is used at a rate of about 0.5 to 30 parts by weight per 100 parts by weight of functionalized olefin polymer. It can, however, be considerably lower with amounts in the vicinity of 0.1 percent being enough to enhance the compatibility of the ground vulcanized rubber particles and the polyolefin resin.
• compositions of this invention various amounts of any number of conventional fillers or compounding ingredients may be admixed.
• ingredients include various carbon blacks, clay, silica, alumina, calcium carbonate, titanium dioxide, pigments, flame retardants, reinforcements, stabilizers, curing agents, anti-oxidants, anti-degradants, tackifiers, processing aids such as lubricants and waxes, plasticizers, etc.
• the amount used depends, at least in part, upon the quantities of the ingredients in the composition.
• a blend composition of the present invention may be manufactured in a single operation or in a number of operational steps.
• the single step operation the vulcanized rubber particles, the functionalized olefin polymer and the polyolefin resin, with the necessary fillers and additives are charged at the desired rates to a suitable mixer, for example, a Banbury internal mixer, two roll mill or extruder, or any device that will allow efficient mixing of the blend at the desired temperature to obtain a composition of the invention.
• a suitable mixer for example, a Banbury internal mixer, two roll mill or extruder, or any device that will allow efficient mixing of the blend at the desired temperature to obtain a composition of the invention.
• a composition of the invention may be prepared by first separately mixing a blend of ground vulcanized rubber and polyolefin resin.
• the independently prepared blend is then melt mixed together with the functionalized olefin polymer in a suitable mixer to obtain a composition of the invention.
• the blending is done at a temperature high enough to soften the polymers for adequate blending, but not so high as to degrade the polymers. Generally speaking, this blending temperature ranges from 140°C to 200°C, and blending is carried out for a time sufficient to homogeneously blend the components.
• the relative proportions of the vulcanized rubber particles, polyolefin resin and the functionalized olefin polymer depend, at least in part, upon the type and molecular weight of the rubber, polyolefin resin and functionalized olefin polymer, and the presence of other ingredients in the composition such as fillers, reinforcements, plasticizers, etc.
• the compositions of the invention comprise about 1-90 parts by weight of ground vulcanized rubber, and correspondingly, about 90-1 parts by weight of polyolefin resin.
• Compositions comprising about 20 to about 80 parts by weight of ground vulcanized rubber, and correspondingly, about 80 to about 20 parts by weight of polyolefin resin are preferred.
• An amount of functionalized olefin polymer which is sufficient to improve the compatibility between the ground vulcanized rubber and the polyolefin resin is satisfactory for the compositions of the invention. Improved compatibility is generally indicated by an increase in elongation or tensile strength or both. An increase in elongation or 25 percent, preferably 50 percent or more, indicates improved compatibility.
• the amount of functionalized olefin polymer required is readily determined by incrementally increasing the amount of functionalized olefin polymer in the blend until the improved properties are observed. Generally, at least 0.5 part by weight of functionalized olefin polymer per 100 parts by weight of polyolefin resin is enough to observe an improvement in compatibility.
• the amount of functionalized olefin polymer is about 0.5 to 50 parts by weight per 100 parts by weight of polyolefin resin. Increasing the amount of functionalized olefin polymer within this range usually increases compatibility. Of course, it is understood that the functionalized olefin polymer may replace all of the polyolefin resin, if desired, but the improvement in properties may not be substantially greater than what is obtained by the use of lesser quantities of functionalized olefin polymer.
• the blend composition of the subject invention are melt processible using conventional plastic processing equipment.
• the properties of the blend depend upon the properties of the components with a wide range of properties being available simply by varying the proportions of the blend components.
• Blends containing high proportion of ground vulcanized rubber are elastoplastic, which means they are elastomeric, but can be processed using conventional plastic processing equipment.
• these components have elongation at break values of 100 to 300 percent without substantial permanent tension set ( i.e., less than 50 percent).
• the melt processability of these compositions allows shaped articles of these compositions to be molded therefrom without the time consuming cure step required with conventional rubbers, thereby reducing finished part cost significantly.
• Blends containing high proportions of polyolefin resin are moldable, rigid thermoplastic compositions exhibiting improved impact resistance. Since in process scrap can be remelted and recycled there is no waste, resulting in additional cost savings.
• the thermoplastic nature of the compositions of the subject invention enables shaped articles made from these compositions to be recycled in the same manner as conventional thermoplastics, thus helping to alleviate the growing environmental problem of solid waste disposal.
• the composition of the subject invention is adaptable to reprocessing of vulcanized rubber from scrap tires and, therefore, it can serve environmental protection by reducing solid waste and the fire/health hazards associated with above-ground storage of tires. Improved compositions of the invention can be used to form a variety of molded, extruded, or calendared articles.
• compositions of the invention include seals and gaskets, automotive parts, anti-skid surfaces, and reinforced hoses. They can be used to coat fabric, industrial belts and various hard surfaces by extrusion coating. They also find utility as impact modifiers for other polymer systems. Compositions within the scope of this invention can be used as the protective covering of reinforced or unreinforced tubes of similar or different compositions.
• the vulcanized rubber particles were obtained by grinding passenger car tires, consisting mainly of SBR rubber. The average particle size was 0.5 mm.
• the rubber particles, functionalized olefin polymer and polyolefin resin were mixed in a Brabender mixer at 100 RPM with the oil bath controlled at 180°C to 190°C for five minutes.
• each batch was placed in a picture frame mold at ambient temperature and compression molded into a sheet 2.0 mm thick in a hydraulic press, both platens of which had been preheated to 200°C. The press was heated for an additional 5 minutes. The molded sheet was then rapidly cooled under pressure to ambient temperature and removed from the press. Test specimens were die cut from the molded sheet and used after 24 hours storage at room temperature. The molded sheet samples were re-melt processible.
• TTB True stress at break
• Extension ratio is the length of a tensile test specimen at break divided by the original, unstressed length of the test specimen. Alternatively, extension ratio is 1.00 plus 1/100 of the percent ultimate elongation.
• Blend compositions are prepared which contain the ingredients in TABLE I.
• Batch A is a control containing unmodified polypropylene.
• Batch B is a control containing unmodified polyethylene.
• Batches C and D illustrate improved compositions of the invention. The data show that the incorporation of a functionalized olefin polymer results in substantial improvement in elongation.
• True stress at break, TSB shows a 2 to 3 fold increase over the controls.
• Example 2 By the same procedure as Example 1, the following compositions were blended (values are in weight percent). This sample serves to illustrate the effect of adding a functionalized olefin polymer containing reactive functional groups such as carboxylic acids.
• Batch A is a control containing unmodified polyethylene.
• Batch C contains an unmodified triblock copolymer consisting of styrene end blocks and poly-(ethylene/butylene) midblocks.
• Batch B contains a copolymer ethylene and methacrylic acid.
• Batch D contains a maleic anhydride functionalized triblock copolymer consisting of styrene end blocks and poly(ethylene/butylene) midblocks.
• Example 2 By the same procedure as Example 1, the following compositions were blended (values in weight percent). This example serves to illustrate the effect of adding compounding ingredients such as lubricants (TABLE V). TABLE V A B C Rubber a 60 60 60 PP b 15 15 15 S(EB)S/2% MA c 25 24 23.9 Zinc stearate d -- 1 1 AC629 e -- -- 0.1 Extrusion rate, 4'' extruder, lbs./hr.
• the barrel temperatures were controlled to obtain a 180°C melt temperature.
• the material was extruded through a sheet die.
• Batches B and C showed better surface appearance than Batch A as a result of better dispersion of the rubber particles.
• the extrusion rate increased significantly and die build up which was present in Batch A was virtually eliminated.
• Batch D of Example 3 was prepared in a 9D Banbury internal mixer at 180°C to 190°C for five minutes.
• the blended composition was pelletized and then fed to a Davis Standard 1 1/2 inch (4.8 cm) diameter extruder with a single stage screw and a length to diameter ratio of 24:1.
• the barrel temperatures were controlled to obtain a 180°C melt temperature.
• the material was extruded through a sheet die.
• This composition in pellet form was also injection molded in a reciprocating type injection molding machine, with all zones of the barrel heated to 170°C and the mold at 25°C. Using an injection pressure of 1000 psi, the molten material filled out the cavity of the plaque mold in 1.5 seconds and was allowed to cool an additional 20 seconds before the mold was opened and the finished part ejected.
• compositions within the scope of this invention can be processed in standard thermoplastic processing equipment and used to fabricate such articles as extruded profiles, tubing, hoses, sheets, etc. or miscellaneous injection molded seals, gaskets, automotive parts or mechanical rubber goods.
• Batch A is a control containing unmodified polyethylene.
• Batch B contains unmodified polyethylene and a dimethylol phenolic resin (SP-1045).
• Batch C contains a vinyl acetate functionalized olefin polymer (EVA).
• Batch D contains a vinyl acetate functionalized olefin polymer (EVA) and a dimethylol phenolic resin (SP-1045).
• the data (Table 6) show a substantial improvement in mechanical properties by the incorporation of a vinyl acetate functionalized olefin polymer and dimethylol phenolic resin.

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• Chemical & Material Sciences (AREA)
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• Chemical Kinetics & Catalysis (AREA)
• Medicinal Chemistry (AREA)
• Polymers & Plastics (AREA)
• Organic Chemistry (AREA)
• Compositions Of Macromolecular Compounds (AREA)
• Processes Of Treating Macromolecular Substances (AREA)
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• Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)

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Citations (5)

• 1995
  • 1995-01-24 CN CN95101349A patent/CN1122345A/zh active Pending
  • 1995-01-26 KR KR1019950001369A patent/KR960017763A/ko not_active Application Discontinuation
  • 1995-01-26 CA CA002141136A patent/CA2141136A1/en not_active Abandoned
  • 1995-02-03 BR BR9500431A patent/BR9500431A/pt not_active Application Discontinuation
  • 1995-03-07 EP EP95103204A patent/EP0710701A1/de not_active Withdrawn
  • 1995-07-24 JP JP7207333A patent/JPH08134223A/ja active Pending

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